EP0623643B1 - Polymeric multinary azanes, process for their preparation and their use - Google Patents
Polymeric multinary azanes, process for their preparation and their use Download PDFInfo
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- EP0623643B1 EP0623643B1 EP94106127A EP94106127A EP0623643B1 EP 0623643 B1 EP0623643 B1 EP 0623643B1 EP 94106127 A EP94106127 A EP 94106127A EP 94106127 A EP94106127 A EP 94106127A EP 0623643 B1 EP0623643 B1 EP 0623643B1
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- multinary
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Definitions
- the sol-gel process has outstanding results in the field of oxidic systems Gaining importance for the production of precursors for glasses and ceramics Materials. It enables the particle size and morphology to be controlled Products obtained are characterized by homogeneous element distribution, high Purity and uniform particle size. It seems desirable this Process also for the synthesis of nitridic or carbonitridic systems use that for some time increasingly for use as ceramic High-performance materials are examined.
- polymeric titaniumazanes are obtained by reacting Ti (NR 2 ) 4 with primary amines.
- J.Am.Ceram.Soc. 71 (1988) 78 shows the ammonolysis of dialkylamides of titanium, niobium or zirconium and the pyrolysis of the polymeric metallazanes obtained to give the corresponding binary nitrides.
- Syntheses of polymeric azanes containing more than one transition metal have so far not been disclosed The synthesis of polymeric multinary azanes has so far only been described for the Si-BN system:
- soluble polyborosilazanes by reacting polysilazanes or polyorganosilanes with organic boron Receive connections.
- DE-A 4107108 discloses the production of oligo or polyborosilazanes by polymerizing heterometallic monomers with Ammonia or alkylamines. However, these methods do not allow the To vary the stoichiometry of the products as desired; the synthesis of the aforementioned heterometallic monomers is also associated with considerable effort.
- the object of the invention is to provide novel, simple and high Yield representable polymeric multinary azanes with adjustable Stoichiometry, which have a homogeneous element distribution, and one Process for the preparation of multinary nitridic and carbonitridic Ceramics made from these polymers.
- polymers which are the subject of this invention.
- the polymers according to the invention are multinary azanes characterized in that the elements E in homogeneous Distribution available.
- the Element distribution uniform up to at least a resolution of 0.5 ⁇ m.
- the inventive ones stand out polymeric multinary azanes with a low chloride content. He is preferably ⁇ 100 ppm, in a particularly preferred embodiment ⁇ 20 ppm.
- the chloride content of the polymers is determined by the Chloride content of the element amides used in the production. Height Chloride levels in the polymers have a negative effect on further processing out. In particular, corrosion occurs to an increased extent during the pyrolysis of the polymers. in the ceramic material cause high chloride content poorer sintering properties and a reduced final density.
- This invention further relates to processes for the preparation of the polymeric multinary azanes according to the invention.
- the reaction is carried out at temperatures between -80 ° C and 200 ° C either in bulk or in an aprotic organic solvent, which can be a C 5 -C 8 alkane, an acyclic or cyclic ether or an alkyl aromatic , where the concentration of the amides is> 0.01m.
- an aprotic organic solvent which can be a C 5 -C 8 alkane, an acyclic or cyclic ether or an alkyl aromatic , where the concentration of the amides is> 0.01m.
- the number and the mixing ratio of the amides used can be as desired be selected so that any desired stoichiometry in terms of the product Elements E can be set.
- the reactivity of the starting materials can be changed in a targeted manner by varying the radicals R 1 and R 2 and selecting a solvent with appropriate donor properties.
- the ammonolysis rates of the amides can be matched and a homogeneous distribution of the elements E in the polymer can thereby be achieved.
- the polymerization rate can be controlled, which makes it easier to control the process conditions during production.
- the properties of the polymers according to the invention can be optimized with regard to further processing.
- R 1 and R 2 are C 1 -C 4 alkanes.
- the viscosity of the solutions can be determined via the concentration of the polymer Solution vary widely and allows optimization of that for the further processing required properties.
- a control of the Degree of crosslinking and the molecular weights of the polymers according to the invention possible. Viscous oils can be obtained at low temperatures, at higher temperatures Temperatures create solids.
- the solvent is preferably reduced Pressure removed.
- Other common ones are also suitable Dry process.
- the invention also relates to the use of the polymeric multinary azanes according to the invention for the production of multinary nitrides or carbonitrides by pyrolysis in an atmosphere containing noble gas, N 2 , NH 3 or primary amines at from 400 to 2000 ° C.
- the polymers are pyrolyzed in the NH 3 stream at temperatures of 400-1000 ° C. for the synthesis of purely nitridic material and then calcined to remove the remaining hydrogen at temperatures between 1400-2000 ° C. in an N 2 or argon atmosphere.
- both steps are carried out under N 2 or Ar.
- the invention also relates to the use of the polymeric multinary azanes according to the invention for the production of ceramic moldings, foils, fibers or coatings by pyrolysis in an inert gas, N 2 , NH 3 or primary amine-containing atmosphere at temperatures of 400 to 2000 ° C.
- polymerization agent enables the properties to be controlled of the polymers according to the invention.
- Analytical data of the polymer infrared spectroscopy [cm -1 ]: 3255 (m); 2960 (s), 2855 (ss, sh), 2760 (s); 2100 (w), 1660 (w), 1575 (m), 1050, 1465, 1400, 1365 (m); 1260 (s); 1095, 1025 (s); 800 (s); , 600 (s, vb). Powder diffractometry: amorphous.
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Abstract
Description
Die vorliegende Erfindung betrifft polymere multinäre Azane, welche aus Baueinheiten der allgemeinen Formel [E(NR1R2)a(NR3)b/2] aufgebaut sind, worin E=B, Al, Ga, In, Si, Ge, Ti, Zr, Hf, V, Nb, Ta, Cr, Mo, W und R1, R2, R3=H, C1-C6-Alkyl, Vinyl, Phenyl sein können, Verfahren zur Herstellung dieser Polymeren sowie deren Verwendung als Vorläuferverbindungen für keramische Hochleistungswerkstoffe.The present invention relates to polymeric multinary azanes which are composed of structural units of the general formula [E (NR 1 R 2 ) a (NR 3 ) b / 2 ], in which E = B, Al, Ga, In, Si, Ge, Ti , Zr, Hf, V, Nb, Ta, Cr, Mo, W and R 1 , R 2 , R 3 = H, C 1 -C 6 alkyl, vinyl, phenyl, process for the preparation of these polymers and their use as a precursor for ceramic high-performance materials.
Im Bereich der oxidischen Systeme hat der Sol-Gel-Prozeß herausragende Bedeutung erlangt für die Herstellung von Precursoren für Gläser und keramische Materialien. Er ermöglicht eine Kontrolle der Teilchengröße und -morphologie, die erhaltenen Produkte zeichnen sich durch homogene Elementverteilung, hohe Reinheit und gleichmäßige Partikelgröße aus. Es erscheint wünschenswert, diesen Prozeß auch für die Synthese nitridischer bzw. carbonitridischer Systeme einzusetzen, die seit einiger Zeit zunehmend für den Einsatz als keramische Hochleistungswerkstoffe untersucht werden.The sol-gel process has outstanding results in the field of oxidic systems Gaining importance for the production of precursors for glasses and ceramics Materials. It enables the particle size and morphology to be controlled Products obtained are characterized by homogeneous element distribution, high Purity and uniform particle size. It seems desirable this Process also for the synthesis of nitridic or carbonitridic systems use that for some time increasingly for use as ceramic High-performance materials are examined.
Bislang sind die Möglichkeiten, durch ein dem Sol-Gel-Prozeß für oxidische Systeme analoges Verfahren polymere Vorläuferverbindungen für keramische Nitride und Carbonitride herzustellen, noch wenig untersucht.So far, the options are through a sol-gel process for oxidic Systems analogous process polymeric precursor compounds for ceramic To produce nitrides and carbonitrides, still little studied.
Gemäß Can.J.Chem 41(1963)134 gelangt man durch Umsetzung von Ti(NR2)4 mit
primären Aminen zu polymeren Titanazanen. Aus J.Am.Ceram.Soc. 71(1988)78
geht die Ammonolyse von Dialkylamiden des Titans, Niobs bzw. Zirkoniums und
die Pyrolyse der erhaltenen polymeren Metallazane zu den entsprechenden binären
Nitriden hervor. Synthesen polymerer Azane, die mehr als ein Übergangsmetall
enthalten, sind bislang nicht bekannt geworden
Die Synthese polymerer multinärer Azane wurde bisher nur für das System Si-B-N
beschrieben:According to Can.J.Chem 41 (1963) 134, polymeric titaniumazanes are obtained by reacting Ti (NR 2 ) 4 with primary amines. From J.Am.Ceram.Soc. 71 (1988) 78 shows the ammonolysis of dialkylamides of titanium, niobium or zirconium and the pyrolysis of the polymeric metallazanes obtained to give the corresponding binary nitrides. Syntheses of polymeric azanes containing more than one transition metal have so far not been disclosed
The synthesis of polymeric multinary azanes has so far only been described for the Si-BN system:
Gemäß den EP-A-389 084 und EP-A-0 424 082 werden lösliche Polyborosilazane durch Umsetzung von Polysilazanen bzw. Polyorganosilanen mit bororganischen Verbindungen erhalten. Die DE-A 4107108 offenbart die Herstellung von Oligo- oder Polyborosilazanen durch Polymerisation heterometallischer Monomere mit Ammoniak bzw. Alkylaminen. Diese Methoden erlauben es jedoch nicht, die Stöchiometrie der Produkte beliebig zu variieren; die Synthese der envähnten heterometallischen Monomere ist zudem mit erheblichem Aufwand verbunden.According to EP-A-389 084 and EP-A-0 424 082, soluble polyborosilazanes by reacting polysilazanes or polyorganosilanes with organic boron Receive connections. DE-A 4107108 discloses the production of oligo or polyborosilazanes by polymerizing heterometallic monomers with Ammonia or alkylamines. However, these methods do not allow the To vary the stoichiometry of the products as desired; the synthesis of the aforementioned heterometallic monomers is also associated with considerable effort.
Aufgabe der Erfindung ist die Bereitstellung neuartiger, einfach und in hohen Ausbeuten darstellbarer polymerer multinärer Azane mit einstellbarer Stöchiometrie, die eine homogene Elementverteilung aufweisen, sowie eines Verfahrens zur Herstellung von multinären nitridischen und carbonitridischen Keramiken aus diesen Polymeren.The object of the invention is to provide novel, simple and high Yield representable polymeric multinary azanes with adjustable Stoichiometry, which have a homogeneous element distribution, and one Process for the preparation of multinary nitridic and carbonitridic Ceramics made from these polymers.
Die Anforderungen werden durch folgende Polymere erfüllt, die Gegenstand dieser Erfindung sind. Es handelt sich dabei um polymere multinäre Azane, welche aus Baueinheiten der allgemeinen Formel [E(NR1R2)a(NR3)b/2] aufgebaut sind, worin E=B, Al, Ga, In, Si, Ge, Ti, Zr, Hf, V, Nb, Ta, Cr, Mo, W und R1, R2, R3=H, C1-C6-Alkyl, Vinyl, Phenyl sein können, dadurch gekennzeichnet, daß mindestens zwei der genannten Elemente E enthalten sind, mit Ausnahme der Kombinationen Si-B und Si-Al, und jedes Atom E von drei bis sechs Stickstoffatomen koordiniert ist, wobei 0≤a≤6, 1≤b≤6, 3≤(a+b)≤6 und a und b ganze Zahlen bedeuten.The requirements are met by the following polymers which are the subject of this invention. These are polymeric multinary azanes which are composed of structural units of the general formula [E (NR 1 R 2 ) a (NR 3 ) b / 2 ], in which E = B, Al, Ga, In, Si, Ge, Ti, Zr, Hf, V, Nb, Ta, Cr, Mo, W and R 1 , R 2 , R 3 = H, C 1 -C 6 alkyl, vinyl, phenyl, characterized in that at least two of the with the exception of the combinations Si-B and Si-Al, and each atom E is coordinated by three to six nitrogen atoms, where 0≤a≤6, 1≤b≤6, 3≤ (a + b) ≤6 and a and b mean integers.
In einer bevorzugten Ausführungsform sind die erfindungsgemäßen polymeren multinären Azane dadurch gekennzeichnet, daß die Elemente E in homogener Verteilung vorliegen. In einer besonders bevorzugten Ausführungsform ist die Elementverteilung bis mindestens zu einer Auflösung von 0.5µm gleichförmig.In a preferred embodiment, the polymers according to the invention are multinary azanes characterized in that the elements E in homogeneous Distribution available. In a particularly preferred embodiment, the Element distribution uniform up to at least a resolution of 0.5µm.
In einer bevorzugten Ausführungsform zeichnen sich die erfindungsgemäßen polymeren multinären Azane einen durch einen niedrigen Chloridgehalt aus. Er beträgt bevorzugt <100 ppm, in einer besonders bevorzugten Ausführungsform <20 ppm. Der Chloridgehalt der Polymeren wird mitbestimmt durch den Chloridgehalt der zur Herstellung verwendeten Elementamide. Hohe Chloridgehalte in den Polymeren wirken sich für die weitere Verarbeitung negativ aus. Insbesondere tritt bei der Pyrolyse der Polymeren verstärkt Korrosion auf. Im keramischen Material verursachen hohe Chloridgehalte schlechtere Sintereigenschaften und eine verringerte Enddichte.In a preferred embodiment, the inventive ones stand out polymeric multinary azanes with a low chloride content. He is preferably <100 ppm, in a particularly preferred embodiment <20 ppm. The chloride content of the polymers is determined by the Chloride content of the element amides used in the production. Height Chloride levels in the polymers have a negative effect on further processing out. In particular, corrosion occurs to an increased extent during the pyrolysis of the polymers. in the ceramic material cause high chloride content poorer sintering properties and a reduced final density.
Gegenstand dieser Erfindung sind weiterhin Verfahren zur Herstellung der erfindungsgemäßen polymeren multinären Azane.This invention further relates to processes for the preparation of the polymeric multinary azanes according to the invention.
Zur Herstellung der erfindungsgemäßen polymeren multinären Azane können Mischungen von Elementamiden der Zusammensetzung E(NR1R2)n, wobei 3≦n≦6, E=B, Al, Ga, In, Si, Ge, Ti, Zr, Hf, V, Nb, Ta, Cr, Mo, W und R1=H, C1-C6-Alkyl, Vinyl, Phenyl, R2=C1-C6-Alkyl, Vinyl, Phenyl bedeuten können, in Substanz oder in einem aprotischen organischen Lösungsmittel mit Ammoniak oder primären Aminen polymerisiert werden.Mixtures of elementamides of the composition E (NR 1 R 2 ) n , where 3 ≦ n ≦ 6, E = B, Al, Ga, In, Si, Ge, Ti, Zr, Hf, V , Nb, Ta, Cr, Mo, W and R 1 = H, C 1 -C 6 alkyl, vinyl, phenyl, R 2 = C 1 -C 6 alkyl, vinyl, phenyl can mean, in bulk or in one aprotic organic solvents are polymerized with ammonia or primary amines.
In einer bevorzugten Ausführungsform wird die Reaktion bei Temperaturen zwischen -80°C und 200°C entweder in Substanz oder in einem aprotischen organischen Lösungsmittel, das ein C5-C8-Alkan, ein acyclischer oder cyclischer Ether oder ein Alkylaromat sein kann, durchgeführt, wobei die Konzentration der Amide >0.01m ist.In a preferred embodiment, the reaction is carried out at temperatures between -80 ° C and 200 ° C either in bulk or in an aprotic organic solvent, which can be a C 5 -C 8 alkane, an acyclic or cyclic ether or an alkyl aromatic , where the concentration of the amides is> 0.01m.
Die Anzahl und das Mischungsverhältnis der eingesetzten Amide kann beliebig gewählt werden, so daß im Produkt jede gewünschte Stöchiometrie bezüglich der Elemente E eingestellt werden kann.The number and the mixing ratio of the amides used can be as desired be selected so that any desired stoichiometry in terms of the product Elements E can be set.
Über die Variation der Reste R1 und R2 und die Auswahl eines Lösungsmittels mit entsprechenden Donoreigenschaften kann die Reaktivität der Edukte gezielt verändert werden. Es lassen sich die Ammonolysegeschwindigkeiten der Amide angleichen und dadurch eine homogene Verteilung der Elemente E im Polymeren erreichen. Des weiteren läßt sich die Polymerisationsgeschwindigkeit steuern, was die Kontrolle der Prozeßbedingungen bei der Herstellung erleichtert. Zudem lassen sich die Eigenschaften der erfindungsgemäßen Polymere im Hinblick auf die Weiterverarbeitung optimieren. In einer bevorzugten Ausführungsform sind R1 und R2 C1-C4-Alkane.The reactivity of the starting materials can be changed in a targeted manner by varying the radicals R 1 and R 2 and selecting a solvent with appropriate donor properties. The ammonolysis rates of the amides can be matched and a homogeneous distribution of the elements E in the polymer can thereby be achieved. Furthermore, the polymerization rate can be controlled, which makes it easier to control the process conditions during production. In addition, the properties of the polymers according to the invention can be optimized with regard to further processing. In a preferred embodiment, R 1 and R 2 are C 1 -C 4 alkanes.
Die Viskosität der Lösungen läßt sich über die Konzentration des Polymeren in Lösung in weiten Bereichen variieren und erlaubt eine Optimierung der für die weitere Verarbeitung benötigten Eigenschaften.The viscosity of the solutions can be determined via the concentration of the polymer Solution vary widely and allows optimization of that for the further processing required properties.
Über die Reaktionstemperatur bei der Polymerisation ist eine Steuerung des Vernetzungsgrads und der Molmassen der erfindungsgemäßen Polymere möglich. Bei niedrigen Temperaturen können viskose Öle erhalten werden, bei höheren Temperaturen entstehen Feststoffe.A control of the Degree of crosslinking and the molecular weights of the polymers according to the invention possible. Viscous oils can be obtained at low temperatures, at higher temperatures Temperatures create solids.
Zur Herstellung von Pulvern wird das Lösungsmittel bevorzugt unter vermindertem Druck entfernt. Geeignet sind auch andere gebräuchliche Trockenverfahren.To produce powders, the solvent is preferably reduced Pressure removed. Other common ones are also suitable Dry process.
Gegenstand der Erfindung ist auch die Verwendung der erfindungsgemäßen polymeren multinären Azane zur Herstellung von multinären Nitriden oder Carbonitriden durch Pyrolyse in Edelgas, N2, NH3 oder primäre Amine enthaltender Atmosphäre bei Temperaturen von 400 bis 2000°C.The invention also relates to the use of the polymeric multinary azanes according to the invention for the production of multinary nitrides or carbonitrides by pyrolysis in an atmosphere containing noble gas, N 2 , NH 3 or primary amines at from 400 to 2000 ° C.
In einer bevorzugten Ausführungsform werden die Polymere zur Synthese von rein nitridischem Material bei Temperaturen von 400-1000°C im NH3-Strom pyrolysiert und anschließend zur Entfernung des restlichen Wasserstoffs bei Temperaturen zwischen 1400-2000°C in N2 oder Argonatmosphäre calciniert. Zur Synthese von carbonitridischem Material führt man beide Schritte unter N2 oder Ar durch.In a preferred embodiment, the polymers are pyrolyzed in the NH 3 stream at temperatures of 400-1000 ° C. for the synthesis of purely nitridic material and then calcined to remove the remaining hydrogen at temperatures between 1400-2000 ° C. in an N 2 or argon atmosphere. For the synthesis of carbonitridic material, both steps are carried out under N 2 or Ar.
Ebenfalls Gegenstand der Erfindung ist die Verwendung der erfindungsgemäßen polymeren multinären Azane zur Herstellung von keramischen Formkörpern, Folien Fasern oder Beschichtungen durch Pyrolyse in Edelgas, N2, NH3 oder primäre Amin enthaltender Atmosphäre bei Temperaturen von 400 bis 2000°C.The invention also relates to the use of the polymeric multinary azanes according to the invention for the production of ceramic moldings, foils, fibers or coatings by pyrolysis in an inert gas, N 2 , NH 3 or primary amine-containing atmosphere at temperatures of 400 to 2000 ° C.
Die Wahl des Polymerisationsagens ermöglicht eine Steuerung der Eigenschaften der erfindungsgemäßen Polymere. Bei Polymerisation mit Ammoniak entstehen unlösliche Duromere, Polymerisation mit primären Aminen führt zu in den gebräuchlichen organischen Lösungsmitteln löslichen Thermoplasten, die direkt in Lösung oder als Schmelze verschiedenen Formgebungsprozessen unterzogen werden können, z.B. Formgießen, Verspinnen zu Fasern, Ziehen von Folien, Herstellung von Beschichtungen durch verschiedene Beschichtungsverfahren wie Tauch- (Dip-Coating) oder Fliehkraftbeschichtung (Spin-Coating).The choice of the polymerization agent enables the properties to be controlled of the polymers according to the invention. Polymerize with ammonia insoluble thermosets, polymerization with primary amines leads to the common organic solvents soluble thermoplastics, which directly in Solution or as a melt subjected to various shaping processes can be e.g. Casting, spinning into fibers, drawing of foils, Production of coatings by various coating processes such as Dip (coating) or centrifugal coating (spin coating).
Im folgenden ist die Erfindung beispielhaft erläutert, ohne daß hierin eine Einschränkung zu sehen ist. The invention is explained by way of example below, without any Restriction can be seen.
Einer Lösung von 8.88 g (0.06 mol) Si(NHCH3)4 und 13.56 g (0.06 mol)
Ti(N(CH3)2)4 in 500 ml Pentan wurden bei -78°C unter Rühren 50 ml NH3
zugegeben. Man ließ die Reaktionsmischung während 12 h auf Raumtemperatur
erwärmen. Das Lösungsmittel wurde unter vermindertem Druck abdestilliert. Es
wurden 12.4 g gelbes Polytitanosilazan erhalten. Analytische Daten des
Polymeren:
Infrarotspektroskopie [cm-1]: 3340 (m); 2920, 2810 (s); 2100 (w); 1550 (w), 1380
(m); 1100 (s); 920 (ss); 550 (m,vb). Pulverdiffraktometrie: amorph.
Energiedisperse Röntgenanalyse: Homogenes Polymer, Verhältnis Si:Ti = 1:1.A solution of 8.88 g (0.06 mol) Si (NHCH 3 ) 4 and 13.56 g (0.06 mol) Ti (N (CH 3 ) 2 ) 4 in 500 ml pentane was added at -78 ° C with stirring 50 ml NH 3 . The reaction mixture was allowed to warm to room temperature over 12 h. The solvent was distilled off under reduced pressure. 12.4 g of yellow polytitanosilazane were obtained. Analytical data of the polymer:
Infrared Spectroscopy [cm -1 ]: 3340 (m); 2920, 2810 (s); 2100 (w); 1550 (w), 1380 (m); 1100 (s); 920 (ss); 550 (m, vb). Powder diffractometry: amorphous. Energy-dispersive X-ray analysis: Homogeneous polymer, Si: Ti ratio = 1: 1.
5 g des Polymeren wurden 12 h lang bei 1000°C im Ammoniakstrom pyrolysiert.
Es wurden 3.1 g eines schwarzglänzenden amorphen Pulvers erhalten,
entsprechend einer keramischen Ausbeute von 62 %. Analytische Daten des
Pyrolyseprodukts:
Infrarotspektroskopie [cm-1]: 3400 (w); 950 (s,b); 470(m,b). Pulverdiffraktometrie:
amorph. Energiedisperse Röntgenanalyse: Homogene Elementverteilung
mindestens bis zur Auflösungsgrenze von 0.5 µm, Verhältnis Si:Ti = 1:1 5 g of the polymer were pyrolyzed in a stream of ammonia at 1000 ° C. for 12 hours. 3.1 g of a black glossy amorphous powder were obtained, corresponding to a ceramic yield of 62%. Analytical data of the pyrolysis product:
Infrared Spectroscopy [cm -1 ]: 3400 (w); 950 (s, b); 470 (m, b). Powder diffractometry: amorphous. Energy-dispersed X-ray analysis: Homogeneous element distribution at least up to the resolution limit of 0.5 µm, ratio Si: Ti = 1: 1
Einer Lösung von 6 g (0.04 mol) Si(NHCH3)4 und 4.5g (0.02 mol) Ti(N(CH3)2)4
in 300 ml Tetrahydrofuran wurden bei -78°C unter Rühren 30 ml NH3 zugegeben.
Man ließ die Reaktionsmischung während 12 h auf Raumtemperatur erwärmen.
Das Lösungsmittel wurde unter vermindertem Druck abdestilliert. Es wurden 7.1 g
gelbes Polytitanosilazan erhalten. Analytische Daten des Polymeren:
Infrarotspektroskopie [cm-1]: 3400 (s); 2920, 2890 (m); 1620 (w); 1460, 1385 (m);
1185 (m); 1040 (ss); 450 (m). Pulverdiffraktometrie: amorph. Energiedisperse
Röntgenanalyse: Homogenes Polymer, Verhältnis Si:Ti = 2:1.30 ml of NH 3 were added to a solution of 6 g (0.04 mol) of Si (NHCH 3 ) 4 and 4.5 g (0.02 mol) of Ti (N (CH 3 ) 2 ) 4 in 300 ml of tetrahydrofuran at -78 ° C. with stirring. The reaction mixture was allowed to warm to room temperature over 12 h. The solvent was distilled off under reduced pressure. 7.1 g of yellow polytitanosilazane were obtained. Analytical data of the polymer:
Infrared Spectroscopy [cm -1 ]: 3400 (s); 2920, 2890 (m); 1620 (w); 1460, 1385 (m); 1185 (m); 1040 (ss); 450 (m). Powder diffractometry: amorphous. Energy-dispersed X-ray analysis: homogeneous polymer, Si: Ti ratio = 2: 1.
5 g des Polymeren wurden 12 h lang bei 1000°C im Ammoniakstrom pyrolysiert.
Es wurden 2.75 g eines schwarzglänzenden amorphen Pulvers erhalten,
entsprechend einer keramischen Ausbeute von 55 %. Analytische Daten des
Pyrolyseprodukts:
Infrarotspektroskopie [cm-1]: 3400 (w); 950 (ss); 460(m,b). Pulverdiffraktometrie:
amorph. Energiedisperse Röntgenanalyse: Homogene Elementverteilung
mindestens bis zur Auflösungsgrenze von 0.5 µm, Verhältnis Si:Ti = 2:1 5 g of the polymer were pyrolyzed in a stream of ammonia at 1000 ° C. for 12 hours. 2.75 g of a black glossy amorphous powder were obtained, corresponding to a ceramic yield of 55%. Analytical data of the pyrolysis product:
Infrared Spectroscopy [cm -1 ]: 3400 (w); 950 (ss); 460 (m, b). Powder diffractometry: amorphous. Energy-dispersed X-ray analysis: Homogeneous element distribution at least up to the resolution limit of 0.5 µm, ratio Si: Ti = 2: 1
Einer Lösung von 7.4 g (0.05 mol) Si(NHCH3)4 in 400 ml Pentan wurden bei
-78°C unter Rühren 50 ml NH3 zugegeben. Nach 5 min wurden 12.8 g (0.05 mol)
Zr(N(CH3)2)4 in 100 ml Pentan zugegeben. Die Reaktionsmischung ließ man
während 12 h auf Raumtemperatur erwärmen und weitere 4 h lang rühren. Das
Lösungsmittel wurde unter vermindertem Druck abdestilliert. Es wurden 11.4g
gelbes Polyzirkonosilazan erhalten. Analytische Daten des Polymeren:
Infrarotspektroskopie [cm-1]: 3350 (s); 2890, 2800 (s); 1470 (w), 1370 (m); 1260
(m); 1100 (ss); 800 (s); 520 (m); 470 (m).
Pulverdiffraktometrie: amorph. Energiedisperse Röntgenanalyse: Homogenes
Polymer, Verhältnis Si:Zr = 1:1.50 ml of NH 3 were added to a solution of 7.4 g (0.05 mol) of Si (NHCH 3 ) 4 in 400 ml of pentane at -78 ° C. with stirring. After 5 minutes, 12.8 g (0.05 mol) of Zr (N (CH 3 ) 2 ) 4 in 100 ml of pentane were added. The reaction mixture was allowed to warm to room temperature over 12 h and stir for a further 4 h. The solvent was distilled off under reduced pressure. 11.4 g of yellow polyzirconosilazane were obtained. Analytical data of the polymer:
Infrared Spectroscopy [cm -1 ]: 3350 (s); 2890, 2800 (s); 1470 (w), 1370 (m); 1260 (m); 1100 (ss); 800 (s); 520 (m); 470 (m).
Powder diffractometry: amorphous. Energy-dispersed X-ray analysis: homogeneous polymer, ratio Si: Zr = 1: 1.
5 g des Polymeren wurden 12 h lang bei 1000°C im Ammoniakstrom pyrolysiert.
Es wurden 2.9 g eines schwarzglänzenden amorphen Pulvers erhalten,
entsprechend einer keramischen Ausbeute von 58 %. Analytische Daten des
Pyrolyseprodukts:
Infrarotspektroskopie [cm-1]: 3400 (w); 950 (s); 530(m). Pulverdiffraktometrie:
amorph.
Energiedisperse Röntgenanalyse: Homogene Elementverteilung mindestens bis zur
Auflösungsgrenze von 0.5 µm, Verhältnis Si:Zr = 1:1 5 g of the polymer were pyrolyzed in a stream of ammonia at 1000 ° C. for 12 hours. 2.9 g of a black glossy amorphous powder were obtained, corresponding to a ceramic yield of 58%. Analytical data of the pyrolysis product:
Infrared Spectroscopy [cm -1 ]: 3400 (w); 950 (s); 530 (m). Powder diffractometry: amorphous.
Energy-dispersed X-ray analysis: Homogeneous element distribution at least up to the resolution limit of 0.5 µm, ratio Si: Zr = 1: 1
Einer Lösung von 10 g (0.067 mol) Si(NHCH3)4 in 400 ml Pentan wurden bei-78°C unter Rühren 50 ml NH3 zugegeben. Innerhalb von 5 min wurde eine Lösung von 4.83 g (0.0335 mol) B(N(CH3)2)3 in 100 ml Pentan zugetropft. Die Reaktionsmischung ließ man während 12 h auf Raumtemperatur erwärmen und weitere 4 h lang rühren. Das Lösungsmittel wurde unter vermindertem Druck abdestilliert. Es wurden 10.3 g weißes Polyborosilazan erhalten. Analytische Daten des Polymeren: Infrarotspektroskopie [cm-1]: 3440 (s); 2890, 2810 (s); 1600 (w); 1460(m); 1360 (m); 1210 (m); 1090, 940 (ss); 800, 470 (m). Pulverdiffraktometrie: amorph.50 ml of NH 3 were added to a solution of 10 g (0.067 mol) of Si (NHCH 3 ) 4 in 400 ml of pentane at -78 ° C. with stirring. A solution of 4.83 g (0.0335 mol) of B (N (CH 3 ) 2 ) 3 in 100 ml of pentane was added dropwise within 5 min. The reaction mixture was allowed to warm to room temperature over 12 h and stir for a further 4 h. The solvent was distilled off under reduced pressure. 10.3 g of white polyborosilazane were obtained. Analytical data of the polymer: infrared spectroscopy [cm -1 ]: 3440 (s); 2890, 2810 (s); 1600 (w); 1460 (m); 1360 (m); 1210 (m); 1090, 940 (ss); 800, 470 (m). Powder diffractometry: amorphous.
5 g des Polymeren wurden 12 h lang bei 1000°C im Ammoniakstrom pyrolysiert. Es wurden 2.8 g eines weißen amorphen Pulvers erhalten, entsprechend einer keramischen Ausbeute von 56 %. Analytische Daten des Pyrolyseprodukts Infrarotspektroskopie [cm-1]: 3400 (w); 1350 (s); 1040 (ss); 460(m). Pulverdiffraktometrie: amorph. 5 g of the polymer were pyrolyzed in a stream of ammonia at 1000 ° C. for 12 hours. 2.8 g of a white amorphous powder were obtained, corresponding to a ceramic yield of 56%. Analytical data of the pyrolysis product infrared spectroscopy [cm -1 ]: 3400 (w); 1350 (s); 1040 (ss); 460 (m). Powder diffractometry: amorphous.
In eine Lösung von 2.13 g (5.6 mmol) Zr(NEt2)4 und 3.19 g (13.1 mmol)
Al(NEt2)3 in 100 ml n-Hexan wurde bei Raumtemperatur NH3 eingeleitet. Es
bildete sich ein fahlgelber Niederschlag, der abfiltriert und unter vermindertem
Druck von anhaftendem Lösungsmittel befreit wurde. Es wurden 1.55 g fahlgelbes
Polyalumozirkonazan erhalten. Analytische Daten des Polymeren:
Infrarotspektroskopie [cm-1]: 3270 (m); 2960, 2920, 2855 (s); 1535 (m); 1460 (m),
1380 (w); 1260 (s); 1095, 1020 (s); 800 (ss); , 600 (s,b). Pulverdiffraktometrie:
amorph.NH 3 was introduced into a solution of 2.13 g (5.6 mmol) of Zr (NEt 2 ) 4 and 3.19 g (13.1 mmol) of Al (NEt 2 ) 3 in 100 ml of n-hexane at room temperature. A pale yellow precipitate formed, which was filtered off and freed of adhering solvent under reduced pressure. 1.55 g of pale yellow polyaluminozirconazane were obtained. Analytical data of the polymer:
Infrared Spectroscopy [cm -1 ]: 3270 (m); 2960, 2920, 2855 (s); 1535 (m); 1460 (m), 1380 (w); 1260 (s); 1095, 1020 (s); 800 (ss); , 600 (s, b). Powder diffractometry: amorphous.
1.5 g des Polymeren wurden 72 h lang bei 990°C im Ammoniakstrom pyrolysiert.
Es wurden 0.8 g eines weißen amorphen Pulvers erhalten, entsprechend einer
keramischen Ausbeute von 53%. Analytische Daten des Pyrolyseprodukts:
Infrarotspektroskopie [cm-1]: 3430 (m); 1635 (m); 1390 (w); 1150 (w); 710 (s,b).
Pulverdiffraktometrie: amorph. Energiedisperse Röntgenanalyse: Homogene
Elementverteilung mindestens bis zur Auflösungsgrenze von 0.5 µm, Verhältnis
Al:Zr ≈ 2:1. 1.5 g of the polymer were pyrolyzed in a stream of ammonia at 990 ° C. for 72 hours. 0.8 g of a white amorphous powder were obtained, corresponding to a ceramic yield of 53%. Analytical data of the pyrolysis product:
Infrared Spectroscopy [cm -1 ]: 3430 (m); 1635 (m); 1390 (w); 1150 (w); 710 (s, b).
Powder diffractometry: amorphous. Energy-dispersive X-ray analysis: Homogeneous element distribution at least up to the resolution limit of 0.5 µm, ratio Al: Zr ≈ 2: 1.
In eine Lösung von 2.92 g (12 mmol) Al(NEt2)3, 2.02 g (6 mmol) Ti(NEt2)4 und
0.76 g (2 mmol) Zr(NEt2)4 in 100ml n-Heptan wurde bei Raumtemperatur NH3
eingeleitet. Es bildete sich ein braunroter Niederschlag, der abfiltriert und unter
vermindertem Druck von anhaftendem Lösungsmittel befreit wurde. Es wurden
2.15 g braunrotes Polyalumotitanozirkonazan erhalten. Analytische Daten des
Polymeren:
Infrarotspektroskopie [cm-1]: 3290 (m); 2960, 2920, 2855 (s); 2000 (w),1550
(s,sh); 1465 (w), 1380 (w); 1260 (s); 1090, 1020 (s); 800 (s); 600 (s,vb).
Pulverdiffraktometrie: amorph.A solution of 2.92 g (12 mmol) of Al (NEt 2 ) 3 , 2.02 g (6 mmol) of Ti (NEt 2 ) 4 and 0.76 g (2 mmol) of Zr (NEt 2 ) 4 in 100 ml of n-heptane was added at room temperature NH 3 initiated. A brown-red precipitate formed, which was filtered off and freed of adhering solvent under reduced pressure. 2.15 g of brown-red polyalumotitanozirconazane were obtained. Analytical data of the polymer:
Infrared Spectroscopy [cm -1 ]: 3290 (m); 2960, 2920, 2855 (s); 2000 (w), 1550 (s, sh); 1465 (w), 1380 (w); 1260 (s); 1090, 1020 (s); 800 (s); 600 (s, vb). Powder diffractometry: amorphous.
2.1 g des Polymeren wurden 72 h lang bei 995°C im Ammoniakstrom pyrolysiert.
Es wurden 1.4 g eines schwarzen amorphen Pulvers erhalten, entsprechend einer
keramischen Ausbeute von 66 %. Analytische Daten des Pyrolyseprodukts:
Infrarotspektroskopie [cm-1]: 3435 (s); 1635 (m); 1400, 1385 (w); 740 (ss,sh).
Pulverdiffraktometrie: amorph. Energiedisperse Röntgenanalyse: Homogene
Elementverteilung mindestens bis zur Auflösungsgrenze von 0.5 µm. 2.1 g of the polymer were pyrolyzed in a stream of ammonia at 995 ° C. for 72 h. 1.4 g of a black amorphous powder were obtained, corresponding to a ceramic yield of 66%. Analytical data of the pyrolysis product:
Infrared Spectroscopy [cm -1 ]: 3435 (s); 1635 (m); 1400, 1385 (w); 740 (ss, sh).
Powder diffractometry: amorphous. Energy-dispersed X-ray analysis: Homogeneous element distribution at least up to the resolution limit of 0.5 µm.
In eine Lösung von 3.37 g (10 mmol) Ti(NEt2)4, 3.70 g (11 mmol) V(NEt2)4 und 4.60 g (12 mmol) Zr(NEt2)4 in 100 ml Tetrahydrofuran wurde bei Raumtemperatur Methylamin eingeleitet. Es bildete sich ein schwarzgrüner Niederschlag, der abfiltriert und unter vermindertem Druck von anhaftendem Lösungsmittel befreit wurde. Es wurden 3.71 g schwarzgrünes Polytitanovanadozirkonazan erhalten. Analytische Daten des Polymeren: Infrarotspektroskopie [cm-1]: 3255 (m); 2960 (s), 2855 (ss,sh), 2760 (s); 2100 (w), 1660 (w), 1575 (m), 1050, 1465, 1400, 1365 (m); 1260 (s); 1095, 1025 (s); 800 (s); , 600 (s,vb). Pulverdiffraktometrie: amorph. In a solution of 3.37 g (10 mmol) of Ti (NEt 2 ) 4 , 3.70 g (11 mmol) of V (NEt 2 ) 4 and 4.60 g (12 mmol) of Zr (NEt 2 ) 4 in 100 ml of tetrahydrofuran was methylamine at room temperature initiated. A black-green precipitate formed which was filtered off and freed of adhering solvent under reduced pressure. 3.71 g of black-green polytitanovanadozirkonazan were obtained. Analytical data of the polymer: infrared spectroscopy [cm -1 ]: 3255 (m); 2960 (s), 2855 (ss, sh), 2760 (s); 2100 (w), 1660 (w), 1575 (m), 1050, 1465, 1400, 1365 (m); 1260 (s); 1095, 1025 (s); 800 (s); , 600 (s, vb). Powder diffractometry: amorphous.
In eine Lösung von 9.7 g (29 mmol) Ti(NEt2)4 und 1.2 g (12mmol) B(NHCH3)3 in 100 ml Heptan wurde bei 90°C NH3 eingeleitet. Es bildete sich ein schwarzer Niederschlag, der abfiltriert und unter vermindertem Druck von anhaftendem Lösungsmittel befreit wurde. Es wurden 3.53 g schwarzes Polytitanoborazan erhalten. Analytische Daten des Polymeren: Infrarotspektroskopie [cm-1]: 3290 (m); 2960, 2920, 2855 (s); 1640 (m); 1380 (w); 1100 (s,b); 600 (m,b). Pulverdiffraktometrie: amorph.NH 3 was introduced at 90 ° C. into a solution of 9.7 g (29 mmol) of Ti (NEt 2 ) 4 and 1.2 g (12 mmol) of B (NHCH 3 ) 3 in 100 ml of heptane. A black precipitate formed, which was filtered off and freed of adhering solvent under reduced pressure. 3.53 g of black polytitanoborazane were obtained. Analytical data of the polymer: infrared spectroscopy [cm -1 ]: 3290 (m); 2960, 2920, 2855 (s); 1640 (m); 1380 (w); 1100 (s, b); 600 (m, b). Powder diffractometry: amorphous.
3.5 g des Polymeren wurden 16 h lang bei 1600°C im Stickstoffstrom pyrolysiert. Es wurden 1.75 g eines schwarzen Pulvers erhalten, entsprechend einer keramischen Ausbeute von 50 %. Analytische Daten des Pyrolyseprodukts: Infrarotspektroskopie [cm-1]: 3435 (s); 1650 (m); 1385 (m); 1150 (m,sh); 800 (w); 660, 600 (w). Pulverdiffraktometrie: weitgehend amorph; einige schwache, sehr breite Peaks deuten auf eine kubische Elementarzelle mit a=4.26Å hin. Energiedisperse Röntgenanalyse: Keine Entmischung beobachtet, homogene Elementverteilung mindestens bis zur Auflösungsgrenze von 0.5 µm. 3.5 g of the polymer were pyrolyzed at 1600 ° C. in a stream of nitrogen for 16 h. 1.75 g of a black powder were obtained, corresponding to a ceramic yield of 50%. Analytical data of the pyrolysis product: infrared spectroscopy [cm -1 ]: 3435 (s); 1650 (m); 1385 (m); 1150 (m, sh); 800 (w); 660, 600 (w). Powder diffractometry: largely amorphous; some weak, very broad peaks indicate a cubic unit cell with a = 4.26Å. Energy-dispersed X-ray analysis: No segregation observed, homogeneous element distribution at least up to the resolution limit of 0.5 µm.
Eine Mischung von 10.47 g (31 mmol) Ti(NEt2)4 und 1.25 g (9 mmol)
B(N(CH3)2)3 wurde unter Ammoniakatmosphäre auf 200°C erhitzt. Es bildeten
sich 2.9 g braunschwarzes Polytitanoborazan. Analytische Daten des Polymeren:
Infrarotspektroskopie [cm-1]:
3290 (m); 2960, 2920, 2855 (s); 1640 (m); 1380 (w); 1100 (s,b); 600 (m,b).
Pulverdiffraktometrie: amorph.A mixture of 10.47 g (31 mmol) of Ti (NEt 2 ) 4 and 1.25 g (9 mmol) of B (N (CH 3 ) 2 ) 3 was heated to 200 ° C. under an ammonia atmosphere. 2.9 g of brown-black polytitanoborazane were formed. Analytical data of the polymer: Infrared spectroscopy [cm -1 ]:
3290 (m); 2960, 2920, 2855 (s); 1640 (m); 1380 (w); 1100 (s, b); 600 (m, b). Powder diffractometry: amorphous.
2.9 g des Polymeren wurden 12 h lang bei 1000°C im Ammoniakstrom pyrolysiert. Es wurden 2.0 g eines schwarzen Pulvers erhalten, entsprechend einer keramischen Ausbeute von 69 %. Analytische Daten des Pyrolyseprodukts: Infrarotspektroskopie [cm-1]: 3440 (s); 1635 (m); 1400, 1385 (m); 1100 (m,sh); 795 (w); 660, 600 (w), 470 (w). Pulverdiffraktometrie: amorph. Energiedisperse Röntgenanalyse: Keine Entmischung beobachtet, homogene Elementverteilung mindestens bis zur Auflösungsgrenze von 0.5 µm. 2.9 g of the polymer were pyrolyzed in a stream of ammonia at 1000 ° C. for 12 hours. 2.0 g of a black powder were obtained, corresponding to a ceramic yield of 69%. Analytical data of the pyrolysis product: infrared spectroscopy [cm -1 ]: 3440 (s); 1635 (m); 1400, 1385 (m); 1100 (m, sh); 795 (w); 660, 600 (w), 470 (w). Powder diffractometry: amorphous. Energy-dispersed X-ray analysis: No segregation observed, homogeneous element distribution at least up to the resolution limit of 0.5 µm.
Eine Mischung von 6.8 g (20 mmol) Ti(NEt2)4 und 5.8 g (40 mmol) B(N(CH3)2)3
wurde unter Methylaminatmosphäre auf 200°C erhitzt. Es bildeten sich 3.40 g
braunschwarzes Polytitanoborazan. Analytische Daten des Polymeren: Infrarotspektroskopie
[cm-1]:
3290 (m); 2960, 2920, 2855 (s); 1640 (m); 1380 (w); 1100 (s,b); 600 (m,b).
Pulverdiffraktometrie: amorph
3.40 g des Polymeren wurden 72 h lang bei 800°C unter Argonatmosphäre
pyrolysiert. Es wurden 1.85 g eines schwarzen Pulvers erhalten, entsprechend einer
keramischen Ausbeute von 55 %. Analytische Daten des Pyrolyseprodukts:
Infrarotspektroskopie [cm-1]: 3425 (s); 1635 (m); 1400, 1385 (s); 1100 (s,sh); 790
(w); 660, 600 (w), 470 (w).
Pulverdiffraktometrie: amorph. Energiedisperse Röntgenanalyse: Keine
Entmischung beobachtet, homogene Elementverteilung mindestens bis zur
Auflösungsgrenze von 0.5 µm.A mixture of 6.8 g (20 mmol) of Ti (NEt 2 ) 4 and 5.8 g (40 mmol) of B (N (CH 3 ) 2 ) 3 was heated to 200 ° C. under a methylamine atmosphere. 3.40 g of brown-black polytitanoborazane were formed. Analytical data of the polymer: Infrared spectroscopy [cm -1 ]:
3290 (m); 2960, 2920, 2855 (s); 1640 (m); 1380 (w); 1100 (s, b); 600 (m, b). Powder diffractometry: amorphous
3.40 g of the polymer was pyrolyzed at 800 ° C. for 72 hours under an argon atmosphere. 1.85 g of a black powder were obtained, corresponding to a ceramic yield of 55%. Analytical data of the pyrolysis product: Infrared spectroscopy [cm -1 ]: 3425 (s); 1635 (m); 1400, 1385 (s); 1100 (s, sh); 790 (w); 660, 600 (w), 470 (w).
Powder diffractometry: amorphous. Energy-dispersed X-ray analysis: No segregation observed, homogeneous element distribution at least up to the resolution limit of 0.5 µm.
Claims (8)
- Polymeric multinary azanes which are built up of structural units of the general formula [E(NR1R2)a(NR3)b/2], where E=B, Al, Ga, In, Si, Ge, Ti, Zr, Hf, V, Nb, Ta, Cr, Mo or W and R1, R2, R3=H, C1-C6-alkyl, vinyl or phenyl, characterized in that at least two of the said elements E are present, with the exception of the combinations Si-B and Si-Al and each atom E is coordinated by from 3 to 6 nitrogen atoms, where 0≤a≤6, 1≤b≤6, 3≤(a+b)≤6 and a and b are integers.
- Polymeric multinary azanes according to Claim 1, characterized in that the elements E are distributed homogeneously.
- Polymeric multinary azanes according to Claim 1 or 2, characterized in that their chloride content is <100 ppm.
- Polymeric multinary azanes according to Claim 3, characterized in that their chloride content is <20 ppm.
- Process for preparing the polymeric multinary azanes according to one or more of Claims 1 to 4, characterized in that mixtures of element amides of the composition E(NR1R2)n, where 3≤n≤6, E=B, Al, Ga, In, Si, Ge, Ti, Zr, Hf, V, Nb, Ta, Cr, Mo or W and R1=H, C1-C6-alkyl, vinyl, phenyl, R2=C1-C6-alkyl, vinyl or phenyl, are polymerized in bulk or in an aprotic organic solvent with ammonia or primary amines.
- Process for preparing the polymeric multinary azanes according to Claim 5, characterized in that the polymerization is carried out at temperatures between -80°C and 200°C, either in bulk or in an aprotic organic solvent which is a C5-C8-alkane, an acyclic or cyclic ether or an alkylaromatic, where the concentration of the amides being >0.01 M.
- Use of the polymeric multinary azanes according to one or more of Claims 1 to 6 for preparing multinary nitrides or carbonitrides by pyrolysis at temperatures of from 400 to 2000°C in an atmosphere containing noble gas, N2, NH3 or primary amines.
- Use of the polymeric multinary azanes according to one or more of Claims 1 to 6 for producing ceramic shaped bodies, films, fibres or coatings by pyrolysis at temperatures of from 400 to 2000°C in an atmosphere containing noble gas, N2, NH3 or primary amine.
Applications Claiming Priority (2)
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---|---|---|---|
DE4314497 | 1993-05-03 | ||
DE4314497A DE4314497A1 (en) | 1993-05-03 | 1993-05-03 | Polymeric multinary azanes, process for their preparation and their use |
Publications (3)
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EP0623643A2 EP0623643A2 (en) | 1994-11-09 |
EP0623643A3 EP0623643A3 (en) | 1995-07-05 |
EP0623643B1 true EP0623643B1 (en) | 1998-12-09 |
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EP94106127A Expired - Lifetime EP0623643B1 (en) | 1993-05-03 | 1994-04-20 | Polymeric multinary azanes, process for their preparation and their use |
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US (1) | US5567832A (en) |
EP (1) | EP0623643B1 (en) |
JP (1) | JPH06340744A (en) |
AT (1) | ATE174362T1 (en) |
DE (2) | DE4314497A1 (en) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
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DE4430817C2 (en) * | 1994-08-30 | 1997-02-13 | Max Planck Gesellschaft | Manufacture of ceramic materials by pyrolysis of highly cross-linked polymeric carbodiimides as ceramic precursors and ceramic precursors |
FR2954318B1 (en) | 2009-12-17 | 2012-02-17 | Univ Claude Bernard Lyon | POLYMETALLOSILAZANE FOR THE PREPARATION OF NANOCOMPOSITES WITH DECORATIVE PROPERTIES, WHICH CAN BE PRESENTED IN THE FORM OF MASSIVE OBJECTS |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
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EP0601405A2 (en) * | 1992-12-08 | 1994-06-15 | Bayer Ag | Polymeric borosilazanes and alumosilazanes and their use |
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US4885576A (en) * | 1986-04-02 | 1989-12-05 | International Business Machines Corporation | Soft copy display of facsimile images |
US4886860A (en) * | 1988-03-23 | 1989-12-12 | Toa Nenryo Kogyo Kabushiki Kaisha | Polymetalosilazane and process for preparing same |
US5030744A (en) * | 1989-03-23 | 1991-07-09 | Tonen Corporation | Polyborosilazane and process for producing same |
US4946809A (en) * | 1989-05-26 | 1990-08-07 | Ultraystems Defense And Space, Inc. | Precursor for A1NBN ceramic and method of use |
JPH0662776B2 (en) * | 1989-08-24 | 1994-08-17 | 信越化学工業株式会社 | Polytitanocarbosilazane polymer and method for producing ceramics using the polymer |
US5171736A (en) * | 1989-10-16 | 1992-12-15 | Massachusetts Institute Of Technology | Preceramic organosilicon-boron polymers |
US5198152A (en) * | 1991-01-15 | 1993-03-30 | Ethyl Corporation | Preceramic compositions and ceramic products with an unsaturated organic or organosilicon compound |
DE4107108A1 (en) * | 1991-03-06 | 1992-09-10 | Bayer Ag | SILICON BORNITRIDE CERAMICS AND PRECURSORS, METHOD FOR THE PRODUCTION AND USE THEREOF |
-
1993
- 1993-05-03 DE DE4314497A patent/DE4314497A1/en not_active Withdrawn
-
1994
- 1994-04-20 AT AT94106127T patent/ATE174362T1/en not_active IP Right Cessation
- 1994-04-20 DE DE59407421T patent/DE59407421D1/en not_active Expired - Fee Related
- 1994-04-20 EP EP94106127A patent/EP0623643B1/en not_active Expired - Lifetime
- 1994-04-25 US US08/231,787 patent/US5567832A/en not_active Expired - Fee Related
- 1994-04-27 JP JP6110150A patent/JPH06340744A/en active Pending
Patent Citations (1)
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EP0601405A2 (en) * | 1992-12-08 | 1994-06-15 | Bayer Ag | Polymeric borosilazanes and alumosilazanes and their use |
Non-Patent Citations (1)
Title |
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Journal of the American Ceramic Society, Bd 71, Nr.1 (1988) , Seiten 78-82. * |
Also Published As
Publication number | Publication date |
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EP0623643A3 (en) | 1995-07-05 |
EP0623643A2 (en) | 1994-11-09 |
US5567832A (en) | 1996-10-22 |
JPH06340744A (en) | 1994-12-13 |
DE59407421D1 (en) | 1999-01-21 |
DE4314497A1 (en) | 1994-11-10 |
ATE174362T1 (en) | 1998-12-15 |
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